US5955011A - Evaporative cooling apparatus and method for a fine fiber production process - Google Patents
Evaporative cooling apparatus and method for a fine fiber production process Download PDFInfo
- Publication number
- US5955011A US5955011A US08/738,941 US73894196A US5955011A US 5955011 A US5955011 A US 5955011A US 73894196 A US73894196 A US 73894196A US 5955011 A US5955011 A US 5955011A
- Authority
- US
- United States
- Prior art keywords
- exhaust gas
- fine fiber
- nozzle
- gas stream
- fine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/02—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of forming fleeces or layers, e.g. reorientation of yarns or filaments
- D04H3/07—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of forming fleeces or layers, e.g. reorientation of yarns or filaments otherwise than in a plane, e.g. in a tubular way
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/06—Manufacture of glass fibres or filaments by blasting or blowing molten glass, e.g. for making staple fibres
Definitions
- the present invention relates to an apparatus for and a method of making and collecting fine fibers, e.g. microfibers, and, in particular, to an apparatus for and a method of making and collecting fine fibers wherein the high energy, high temperature gas streams carrying the fine fibers are cooled, without wetting the fine fibers, to reduce the temperatures at and surrounding the primary and secondary fine fiber collection equipment used in the process.
- fine fibers e.g. microfibers
- the present invention relates to an apparatus for and a method of making and collecting fine fibers, e.g. microfibers, and, in particular, to an apparatus for and a method of making and collecting fine fibers wherein the high energy, high temperature gas streams carrying the fine fibers are cooled, without wetting the fine fibers, to reduce the temperatures at and surrounding the primary and secondary fine fiber collection equipment used in the process.
- Fine fibers such as microfibers having mean diameters between about 0.5 and 2.0 microns and other fine fibers having mean diameters of about 7 microns or less, are made from glass, high temperature resistant ceramic materials, organic (carbon based) materials, polymers and other fiberizable materials. These fine fibers are typically made by a process, such as a flame attenuation process, wherein filaments or fibers are heated and attenuated by a high energy hot gaseous blast and carried by a gaseous stream of combustion gases and inspirated air to a collection surface where the fine fibers are separated from the gaseous stream and collected on the collection surface. Typically, the fine fibers are collected as a mat of randomly oriented fibers which is later removed from the collection surface and delivered to a windup mandrel or pneumatic conveying system for packaging or further processing.
- One flame attenuation process used to form such fine fibers involves the formation of continuous, relatively large diameter filaments which are formed by pulling the filaments from fiberizing orifices in the bottom of a heated pot or melter, containing a molten fiberizable material, by pull rolls.
- the continuous filaments are then fed into the hot, high energy gaseous blast of a burner where the continuous, relatively large diameter filaments are attenuated, formed into discrete length fibers, and carried through forming tubes toward a primary fine fiber collection equipment by the combustion gases from the burner and inspirated air.
- the primary fine fiber collection equipment is a rotating metallic collection drum with a perforated, cylindrical collection surface.
- a negative pressure is created within the rotating metallic collection drum by means of an exhaust system, connected to the interior of the collection drum, which withdraws gases from the interior of the collection drum.
- the negative pressure within the collection drum draws the gases of the fine fiber containing gaseous stream through the perforations in the collection surface thereby separating the gases from most of the fine fibers in the gaseous stream which are collected into a mat of randomly oriented fibers on the primary collection surface.
- the mat of fine fibers is subsequently removed from the primary collection surface by a doffing and smooth roll assembly and delivered to a windup mandrel or a pneumatic conveying system for packaging or further processing.
- the exhaust gases from the primary collection equipment carrying fine fibers not removed from the gasses by the primary collection equipment, have been passed through wet scrubber exhaust gas abatement equipment to remove fine fibers from the exhaust gases and clean the exhaust gases.
- the cleaned gases were then discharged to the atmosphere through an exhaust stack.
- wet scrubbers as exhaust gas abatement equipment in a fine fiber production process, causes a number of problems.
- the volume of air and combustion gases passing through the primary collection equipment and into the exhaust system to be cleaned by the exhaust gas abatement equipment ranges from about 20,000 to about 60,000 ACFM (actual cubic feet per minute).
- a wet scrubber used as the exhaust gas abatement equipment in such a process must be operated at a high pressure drop across the scrubber, about 16 inches of water column, to achieve a filtration efficiency of about 90% for fiber five microns in diameter and above.
- the operation of a wet scrubber in such a process is expensive.
- fine fibers such as glass microfibers, are hydrophilic and once these fibers are wetted by the scrubber, the fibers are no longer useable in a product and become scrap.
- Another problem associated with the use of a wet scrubber to clean exhaust gases in a fine fiber production process is the creation of clumps of wet fibers in the exhaust system which can be discharged through the exhaust stack.
- the water used in a wet scrubber absorbs volatiles from the exhaust gases and becomes waste water which must be treated and from an aesthetic point of view, the steam discharged from the exhaust stack of the process can be unsightly.
- the process In fine fiber production processes, such as the flame attenuation process discussed above, not only does the process have to handle large volumes of gases, e.g from about 20,000 to about 60,000 ACFM traveling at speeds of up to about 500 feet per minute, but the ambient or surrounding temperature in the fine fiber collection chamber at the primary collection equipment, due to the high temperatures of the combustion gases typically ranges from about 350° F. to about 550° F. and the temperatures of the exhaust gases passing from the primary collection equipment to the exhaust gas abatement equipment ranges from about 300° F. to about 500° F. The temperatures are typically at the higher end of the ranges in the hotter summer months.
- gases e.g from about 20,000 to about 60,000 ACFM traveling at speeds of up to about 500 feet per minute
- the ambient or surrounding temperature in the fine fiber collection chamber at the primary collection equipment due to the high temperatures of the combustion gases typically ranges from about 350° F. to about 550° F. and the temperatures of the exhaust gases passing from the primary collection equipment to the exhaust gas abatement equipment ranges from about 300°
- the evaporative cooling apparatus and method of the present invention solve the above discussed problems by providing a way of cooling the gases in the process, without wetting the fine fibers, so that the temperatures of the fine fiber containing gaseous stream of combustion gases and inspirated air impacting the primary collection equipment and of the exhaust gases being cleansed by the exhaust gas abatement equipment are both reduced.
- the fine fiber containing high energy, high temperature gaseous streams of combustion gases and inspirated air are cooled by evaporative cooling before the gaseous streams impact the primary fine fiber collection surface or filter media of the primary fine fiber collection equipment.
- the gaseous stream is cooled as it passes from the fiber forming equipment to the primary fine fiber collection equipment through forming tubes.
- Water spray nozzles shielded from the gaseous streams by nozzle scoops, spray water into the gaseous streams without wetting the fine fibers or the inner surfaces of the forming tubes.
- clumps of wet fibers do not build up on the nozzles or on the inner surfaces of the forming tubes to be later carried away by the gaseous streams to impact against the primary collection surface or filter media where the clumps would clog the perforations in the collection surface or the filter media and ruin the product.
- the nozzle scoops also create a venturi effect within the forming tubes adjacent the spray nozzles to draw air into the forming tubes through the nozzle ports where the nozzles are located.
- the air, inspirated into the forming tubes through these ports, also prevents fibers from the gaseous stream from collecting into clumps on the nozzles.
- the droplets of the nozzle sprays are sized so that the droplets evaporate before impacting the primary fine fiber collection surface or filter media so that the collection surface or filter media are not wetted. Any wetting of the collection surface or filter media would also cause the fine fibers to form into clumps thereby clogging the perforations in the collection surface or the interstices of the filter media and ruining the product.
- the evaporative cooling of the fine fiber containing gaseous stream carrying the fine fibers to the primary collection equipment reduces the temperatures surrounding the primary fine fiber collection equipment and the exhaust gases removed from the primary fine fiber collection equipment and passed through the exhaust gas abatement equipment.
- the operating temperatures for both the primary fine fiber collection equipment and the exhaust gas abatement equipment are reduced thereby prolonging the service life of such equipment and improving the efficiency of the production process.
- the exhaust gases from the primary fine fiber collection equipment, carrying fine fibers not collected by the primary fine fiber collection equipment, are cooled by evaporative cooling prior to being introduced into the exhaust gas abatement equipment.
- the exhaust gases are cooled as they flow from the primary fine fiber collection equipment to the exhaust gas abatement equipment through an exhaust duct.
- One or more, preferably a plurality, water spray nozzles each shielded from the exhaust gas stream by a nozzle scoop, spray water into the exhaust gas stream without wetting the fine fibers or the inner surface of the exhaust duct.
- clumps of wet fibers do not build up on the nozzle or nozzles or on the inner surface of the exhaust duct to be later carried away by the exhaust gas stream to impact against the filter media of the exhaust abatement equipment where the clumps would clog the fibrous filter media.
- the nozzle scoop or scoops also create a venturi effect within the exhaust duct adjacent the spray nozzles to draw air into the exhaust duct through the nozzle ports where the nozzles are located.
- the air inspirated into the exhaust duct through these ports also prevents fibers in the exhaust gas stream from collecting into clumps on the nozzles.
- the droplets of the sprays from the nozzles are sized so that the droplets evaporate before impacting the filter media of the exhaust gas abatement equipment so that the filter media is not wetted. Any wetting of the filter media would also cause the fine fibers to form into clumps or wads on the filter media thereby clogging the interstices of the filter media.
- the evaporative cooling of the fine fiber containing exhaust gas stream reduces the temperatures surrounding the exhaust gas abatement equipment.
- the gases passing through the fine fiber forming process are drawn through the process by an exhaust fan or fans in the exhaust gas system located downstream of the location where the exhaust gases are cooled, for a constant volume of gases passing through the exhaust fan or fans more air mass will be inspirated into the combustion gases and air passing through the primary fine fiber collection equipment thereby cooling the primary fine fiber collection equipment.
- the operating temperatures for both the primary fine fiber collection equipment and the exhaust gas abatement equipment are reduced thereby prolonging the service life of such equipment and improving the efficiency of the production process.
- both the gaseous stream of combustion gases and air carrying the fine fibers to the primary fine fiber collection equipment and the exhaust gas stream carrying fine fibers, not removed from the gases by the primary fine fiber collection equipment, to the exhaust gas abatement equipment (the secondary fine fiber collection equipment) are cooled by evaporative cooling.
- FIG. 1 is a schematic view of the fine fiber forming process of the present invention with evaporative cooling equipment in the forming tubes and the exhaust duct of the process.
- FIG. 2 is a schematic side view of a forming tube with the evaporative cooling equipment of the present invention.
- FIG. 3 is an end view of the forming tube of FIG. 2, taken substantially along lines 3--3 of FIG. 2.
- FIG. 4 is a schematic side view of a preferred forming tube with the evaporative cooling equipment therein.
- FIG. 5 is an end view of the forming tube of FIG. 2, taken substantially along lines 3--3 of FIG. 2.
- FIG. 6 is a schematic view, from the inside of a forming tube or exhaust duct, of the nozzle scoop and spray nozzle of the evaporative cooling equipment used in the apparatus and method of the present invention.
- FIG. 7 is a side schematic view of the nozzle scoop and spray nozzle of the evaporative cooling equipment used in the apparatus and method of the present invention.
- FIG. 8 is a schematic side view of a preferred installation of the evaporative cooling equipment in the exhaust duct.
- a flame attenuation, fine fiber forming production line 20, employing the evaporative cooling system and method of the present invention includes: fine fiber forming equipment 22; a series of forming tubes 24; a collection chamber 26 enclosing a primary fine fiber collection drum 28; a doffing and smooth roll assembly 32 for removing fine fibers from the collection drum 28 and delivering the fine fibers to a windup mandrel or pneumatic conveying system (not shown) for packaging or further processing; an exhaust duct 34; exhaust gas abatement equipment 36; an exhaust fan 38; and an exhaust stack 40.
- the forming tubes are provided with an evaporative cooling system 42 and the exhaust duct 34 is provided with an evaporative cooling system 44.
- the fine fiber forming equipment 22, shown in FIG. 1, includes melters or pots 46 which are typically heated with a gas burner or electrical heating elements to maintain the fiberizable material within the melters or pots 46 at an appropriate fiberizing temperature.
- the bottom walls of the melters or pots 46 are each provided with a large number of fiberizing orifices from which relatively large diameter continuous filaments 48, commonly referred to as primary filaments, are pulled or drawn by driven pull rolls 50. After passing through the pull rolls 50, the continuous filaments 48 are introduced into the flames of flame attenuation burners 52, e.g. Selas or similar burners.
- the high energy, high temperature flames of the flame attenuation burners 52 attenuate the filaments 48 and form fine fibers which are carried by the combustion gases into and through the forming tubes 24 to impact against the perforated collection drum 28 within the collection chamber 26. While the fine fiber forming process shown in FIG. 1 is one type of a flame attenuation process, the fine fibers can also be formed by flame attenuation rotary or similar fiberization processes.
- the fine fibers made by these processes have mean diameters of about 7 microns or less and are made of glass, high temperature resistant ceramic materials, polymers, organic (carbon based) materials or other suitable fiberizable materials. Processes, such as the one shown in FIG. 1, are especially suited for forming and collecting very fine fibers called microfibers which are normally very difficult to collect. Microfibers have mean diameters between about 0.5 microns and 2 microns and have aspect ratios of length to diameter of about 10 ⁇ to about 10,000 ⁇ . However, these processes are also well suited for forming and collecting fine fibers having mean diameters between about 0.5 microns and 7 microns and aspect ratios of length to diameter of 10 ⁇ and greater.
- the fiber collection drum 28 is a rotating tubular drum typically about six feet in diameter by about eight feet in length and has a perforated metal cylindrical collection surface that functions as the primary fine fiber collection surface for the process, such as drums marketed by Continental Corporation.
- the doffing and smooth roll assembly 32 removes the collected fine fibers from the perforated collection surface of the drum and delivers the fine fibers to a windup mandrel or pneumatic conveying system (not shown) for packaging or further processing. While this is a preferred means of collecting the fine fibers, other fine fiber collection surfaces or filter media, capable of effectively and efficiently removing low concentrations of fine fibers from a high energy, high temperature gaseous stream and collecting such fibers for packaging or further processing can also be used as the primary fine fiber collection equipment.
- the distance from the fiber attenuation zone of the fine fiber forming equipment 22 to the collection surface of the fine fiber collection drum 28 is typically quite short, about 10-12 feet, and the fine fiber containing gaseous stream of combustion gases and inspirated air typically travels at velocities of up to about 500 feet per minute and temperatures from about 350° F. and 550° F.
- the volumes of combustion gases and inspirated air passing though the collection surface of the collection drum, to collect about 50 to 150 pounds of fine fibers per hour, ranges from about 20,000 to about 60,000 ACFM.
- the fiber containing gaseous streams of the combustion gases and inspirated air for six forming tubes were cooled using one spray nozzle per forming tube and a total of 1.1 gallons/minute of cooling water for the six forming tubes.
- the evaporative cooling equipment of the present invention reduced the temperatures at the collection drum from 434° F. to 399° F, a drop of 35° F., and no wet fiber wad formation was observed.
- the exhaust fan 38 of the exhaust system withdraws or pulls gases (the combustion gases and inspirated air) from the interior of the rotating collection drum 28 through the exhaust duct 34 to a chamber housing the exhaust gas abatement equipment 36 and through the exhaust gas abatement equipment, where fine fibers in the exhaust gases are removed from the exhaust gases, before the exhaust gasses are discharged out through the exhaust stack 40.
- the exhaust fan 38 is a conventional, commercially available exhaust fan with a capacity at least equal to the maximum volume of gases to be passed through the fine fiber forming process.
- the exhaust gas abatement equipment 36 is a conventional dry drum exhaust gas abatement apparatus which can remove fine fibers from an exhaust gas stream, such as dry drum filtration equipment sold by Osprey Corporation or Continental Corporation.
- the dry drum filtration equipment includes a rotating drum filter 54, about ten feet in diameter by about nineteen feet long, which carries a filter media 56 on its cylindrical collection surface for removing fine fibers from the exhaust gas stream passing through the filter media.
- the filter media 56 As the drum filter 54 rotates the filter media 56 is passed by vacuum nozzles 58 of a vacuum system which remove the fine fibers from the filter media 56 and pneumatically convey the fine fibers into a conventional cyclone separator or similar means (not shown) where the fine fibers are separated from the gases and collected for packaging or further processing.
- the exhaust gases passing from the collection drum to the exhaust gas abatement equipment were evaporatively cooled using four spray nozzles and a total of four gallons/minute of water.
- the temperature at the exhaust gas abatement equipment was reduced from 320° F. to 250 F., a reduction of 70° F., and no wet fiber wad formation was observed.
- the temperature of the fiber containing stream of combustion gases and inspirated air at the collection drum was reduced by 11° F. from 345° F. to 334° F.
- the forming tubes 24 used in the process can have a constant diameter with a constricted inlet opening 60, as schematically shown in FIGS. 1-3, the preferred configuration for the forming tubes 24' is shown in FIGS. 4 and 5.
- the forming tube 24' has a constricted section 62 which has the same size and cross sectional shape as or essentially the same size and cross sectional shape as inlet opening 60; an outlet section 64 which is the same diameter as the forming tube 24; and an expansion section 66 which connects the constricted section 62 with the outlet section 64.
- the preferred forming tube design minimizes gas stream turbulence adjacent the evaporative cooling system 42 to prevent fine fiber buildup on the water spray nozzle 68 of the evaporative cooling system 42. While the transverse cross section of the forming tubes 24 and 24' are shown as essentially round, the transverse cross section of the forming tubes can be square, rectangular, oval, flat oval or other configurations.
- the evaporative cooling system 42 for the forming tubes 24 or 24' includes the water spray nozzle 68, a nozzle insertion port 70, and an aerodynamic nozzle shield or scoop 72 for shielding the nozzle 68 from the gas stream carrying the fine fibers.
- the nozzle insertion port 70 is larger in diameter than the water spray nozzle 68 so that outside air can be inspirated into the forming tubes through the nozzle insertion port 70 to prevent fine fibers, carried by the gas stream, from attaching to the nozzle and forming a wad of fibers that can interfere with the spray pattern of the nozzle and later be detached and carried by the gas stream to the collection surface where it could plug or clog the perforations in the collection surface.
- the downstream end of the nozzle shield or scoop 72 is preferably located immediately upstream of the nozzle insertion port 70.
- the upstream portion 74 of the nozzle shield or scoop 72 has a generally conical surface which expands in the downstream direction and merges into a downstream portion 76 of the nozzle shield or scoop which has a generally cylindrical surface.
- the transverse curvature of the nozzle shields or scoops 72 can have other, preferably aerodynamic, curvatures or shapes, such as, but not limited to oval curvatures, flattened oval curvatures and the like. While not preferred, it is also contemplated that the nozzle shields or scoops 72 could have a generally rectangular transverse cross section, expanding in the downstream direction, with rounded corners. By way of example, for a forming tube about sixteen inches in diameter, the nozzle shield 72 is typically about eight inches long and about two inches deep at its downstream end.
- the water spray nozzle 68 is selected to provide a spray of very fine droplets e.g. about 30 microns or less in size, which will evaporate in the gas stream before impacting the collection surface so that the water from the spray does not wet the fine fibers in the gas stream or the collection surface of the collection drum 28.
- Various nozzles may be used such as, but not limited to, high pressure (e.g. about 1000 psi) hydraulic nozzles; air atomized hydraulic nozzles (e.g. water about 80 psi and air about 40 psi); and air atomized hydraulic nozzles of the type just identified with ultra-sonic resonator caps at the nozzle exit to further shatter the water droplets.
- the pattern of the spray emitted by the nozzle 68 is selected to avoid contact with the inside surface of the forming tubes 24 or 24' so that the inside surface of the forming tube 24 or 24' does not become wet. If the inside surface of the forming tube 24 or 24' becomes wet, fine fibers will become wet, stick to the surface and buildup into a wet wad or clump of fine fibers on the surface. At a certain point in its growth, the wet wad or clump of fine fibers will be detached from the inside surface of the forming tube by the gas stream and carried to the collection surface of the collection drum 28 where the wad or clump of wet fibers can clog the perforations in the collection surface.
- the nozzle used is selected to have a spray pattern which is widest at the opposed diameter of the forming tube. While the evaporative cooling system has been described in terms of one nozzle, insertion port and nozzle shield assembly per forming tube 24 or 24', which is the preferred system, additional nozzle, insertion port and nozzle shield assemblies can be included in the forming tubes 24 and 24' if necessary.
- the fine fiber containing gas stream of burner combustion gases and inspirated air pass into the inlet openings of the forming tubes 24 or 24'; past the evaporative cooling systems 42; and out the discharge ends of the forming tubes 24 or 24' where the gas streams impact the primary fine fiber collection surface of the collection drum 28.
- the constricted sections 62 of the forming tubes permit the gas streams of combustion gases and inspirated air to establish a more laminar flow, than the gas streams in forming tubes 24, to minimize turbulence within the forming tubes that could carry fine fibers from the gas streams into contact with the water spray nozzles 68 where the fine fibers could form into a wad.
- the expansion sections 66 of the forming tubes 24' cause a rapid expansion of the gases in the gas streams to further increase the negative pressure present within the forming tubes 24' and draw outside air into the forming tubes 24' through the nozzle insertion ports 70.
- the nozzle shields or scoops 72 directly shield the nozzles 68 from the gas streams and also create a venturi effect within the forming tubes 24 or 24' to draw air into the forming tubes through the nozzle insertion ports 70.
- the flow of air into the forming tubes 24 or 24' through the nozzle insertion ports 70 and around the nozzles 68 further acts to keep fine fibers in the gas streams from coming into contact with the nozzles 68.
- the nozzles 68 emit sprays of fine water droplets into the streams of combustion gases and inspirated air which evaporate in the gas streams of combustion gases and inspirated air before the gas streams reach the primary collection surface.
- the evaporation of the water droplets cools the gas streams to reduce the temperatures surrounding the collection drum 28 in the collection chamber 26 thereby prolonging the service life of seals, doffing roll flights and other components of the collection drum which are more susceptible to deterioration at high operating temperatures.
- the cooling of the gas streams in the forming tubes 24 or 24' also reduces the temperature of the exhaust gases withdrawn from the collection drum 28 and passed through the exhaust gas abatement equipment 36 thereby prolonging the service life of the filter media and other temperature sensitive components of the drum filter.
- the evaporative cooling system 44 located in the exhaust duct 34 includes the water spray nozzle 68, a nozzle insertion port 70, and an aerodynamic nozzle shield or scoop 72 for shielding the nozzle 68 from the exhaust gas stream carrying the fine fibers.
- the nozzle insertion port 70 is larger in diameter than the water spray nozzle 68 so that outside air can be inspirated into the exhaust duct 34 through the nozzle insertion port 70 to prevent fine fibers, carried by the exhaust gas stream, from attaching to the nozzle and forming a wad of fibers that can interfere with the spray pattern of the nozzle and later be detached and carried by the gas stream to the dry drum filter where it could plug or clog the filter media of the filter drum.
- the downstream end of the nozzle shield or scoop 72 of the evaporative cooling system 44 is preferably located immediately upstream of the nozzle insertion port 70.
- the upstream portion 74 of the nozzle shield or scoop 72 has a generally conical surface which expands in the downstream direction and merges into a downstream portion 76 of the nozzle shield or scoop which has a generally cylindrical surface.
- the nozzle shields or scoops 72 used in the evaporative cooling system 44 can have other, preferably aerodynamic, curvatures or shapes, such as, but not limited to oval curvatures, flattened oval curvatures and the like.
- the nozzle shields or scoops 72 could have a generally rectangular transverse cross section, expanding in the downstream direction, with rounded corners.
- the nozzle shield 72 used in the evaporative cooling system 44 is about eight inches long and about two inches deep at its downstream end.
- the water spray nozzle 68 for the evaporative cooling system 44 is selected to provide a spray of very fine droplets e.g. about 170 microns or less in size, which will evaporate in the exhaust gas stream before impacting the filter media 56 of the filter drum 54 so that the water from the spray does not wet the fine fibers in the exhaust gas stream or the filter media 56 of the filter drum 54.
- the evaporative cooling system 44 may used various nozzles such as, but not limited to, high pressure (e.g. about 1000 psi) hydraulic nozzles; air atomized hydraulic nozzles (e.g.
- the pattern of the spray emitted by the nozzle 68 is selected to avoid contact with the inside surface of the exhaust duct 34 so that the inside surface of the exhaust duct does not become wet. If the inside surface of the exhaust duct becomes wet, fine fibers will become wet, stick to the surface and buildup into a wet wad or clump of fine fibers on the surface.
- the wet wad or clump of fine fibers will be detached from the inside surface of the exhaust duct by the exhaust gas stream and carried to the filter media 56 of the filter drum 54 where the wad or clump of wet fibers can clog the interstices in the filter media 56.
- the exhaust duct typically has a rectangular cross section and is larger in size than the forming tubes 24 or 24'. Accordingly, there are typically one, two, three or more additional nozzle, insertion port and nozzle shield assemblies located in the exhaust duct 34.
- the exhaust duct 34 may have other than a rectangular transverse cross section, such as but not limited to, round, oval, flat oval and square.
- each of the nozzle, insertion port and nozzle shield assemblies are located on a different wall of the exhaust duct or are equally spaced around the exhaust duct at the same location along the longitudinal axis of the exhaust duct 34.
- the exhaust duct 34 has an expansion section 80 therein.
- the expansion section 80 is typically much larger in diameter than the exhaust duct 34 in general, e.g. seven feet in diameter vs four feet in diameter, and includes an upstream expansion portion 82 and a downstream reduction portion 84.
- the water spray nozzle, nozzle insertion port and aerodynamic nozzle shield or scoop assemblies are preferably located adjacent the upstream expansion portion 82 of the expansion section 80.
- the expansion section 80 causes a rapid expansion of the gases in the exhaust gas stream to further increase the negative pressure present within the exhaust duct and draw outside air into the exhaust duct 34 through the nozzle insertion ports 70.
- the exhaust gas stream containing fine fibers not collected by the primary collection surface of the collection drum 28 pass from the collection drum into the exhaust duct 34, past the evaporative cooling system 44, through the exhaust gas abatement equipment 36 and out the exhaust stack 40.
- the nozzle shields or scoops 72 directly shield the nozzles 68 of the evaporative cooling system 44 from the exhaust gas stream and also create a venturi effect within the exhaust duct 34 to draw air into the exhaust duct through the nozzle insertion ports 70.
- the flow of air into the exhaust duct through the nozzle insertion ports 70 and around the nozzles 68 further acts to keep fine fibers in the exhaust gas stream from coming into contact with the nozzles 68.
- the nozzles 68 emit sprays of fine water droplets into the exhaust gas stream which evaporate in the exhaust gas stream before the exhaust gas stream impacts the filter media 56 of the filter drum 54 (the secondary fine fiber collection media).
- the evaporation of the water droplets cools the exhaust gas stream to reduce the temperatures surrounding the filter drum 54 and thereby prolong the service life of the filter media (typically a fibrous filter media), seals, and other components of the exhaust gas abatement equipment 36 which are more susceptible to deterioration at high operating temperatures.
- both evaporative cooling systems 42 and 44 When both evaporative cooling systems 42 and 44 are used together, the cooling effects of both systems can be combined to cool the operating temperatures surrounding both the collection drum 28 and the exhaust gas abatement equipment 36 without wetting the fibers so that there can be a primary and a secondary collection of the fine fibers in the process.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
Claims (26)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/738,941 US5955011A (en) | 1996-10-24 | 1996-10-24 | Evaporative cooling apparatus and method for a fine fiber production process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/738,941 US5955011A (en) | 1996-10-24 | 1996-10-24 | Evaporative cooling apparatus and method for a fine fiber production process |
Publications (1)
Publication Number | Publication Date |
---|---|
US5955011A true US5955011A (en) | 1999-09-21 |
Family
ID=24970143
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US08/738,941 Expired - Lifetime US5955011A (en) | 1996-10-24 | 1996-10-24 | Evaporative cooling apparatus and method for a fine fiber production process |
Country Status (1)
Country | Link |
---|---|
US (1) | US5955011A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1249181A2 (en) * | 2001-04-10 | 2002-10-16 | British American Tobacco (Germany) GmbH | Treatment of process gas for a tobacco dryer |
US20050106970A1 (en) * | 2000-09-01 | 2005-05-19 | Stanitis Gary E. | Melt processable perfluoropolymer forms |
US20050163968A1 (en) * | 2004-01-20 | 2005-07-28 | Hanket Gregory M. | Microfiller-reinforced polymer film |
US20070137259A1 (en) * | 2005-12-21 | 2007-06-21 | Borders Harley A | Processes and systems for making inorganic fibers |
US20100147033A1 (en) * | 2006-01-10 | 2010-06-17 | Terry Joe Hanna | Method of fiberizing molten glass |
US20140076000A1 (en) * | 2012-09-20 | 2014-03-20 | Timothy James Johnson | Apparatus and method for air flow control during manufacture of glass fiber insulation |
US11572645B2 (en) * | 2017-09-01 | 2023-02-07 | Paroc Group Oy | Apparatus and method for manufacturing mineral wool as well as a mineral wool product |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3902878A (en) * | 1971-05-21 | 1975-09-02 | Owens Corning Fiberglass Corp | Method and apparatus for producing fibers and environmental control therefor |
US3959421A (en) * | 1974-04-17 | 1976-05-25 | Kimberly-Clark Corporation | Method for rapid quenching of melt blown fibers |
-
1996
- 1996-10-24 US US08/738,941 patent/US5955011A/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3902878A (en) * | 1971-05-21 | 1975-09-02 | Owens Corning Fiberglass Corp | Method and apparatus for producing fibers and environmental control therefor |
US3959421A (en) * | 1974-04-17 | 1976-05-25 | Kimberly-Clark Corporation | Method for rapid quenching of melt blown fibers |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050106970A1 (en) * | 2000-09-01 | 2005-05-19 | Stanitis Gary E. | Melt processable perfluoropolymer forms |
EP1249181A2 (en) * | 2001-04-10 | 2002-10-16 | British American Tobacco (Germany) GmbH | Treatment of process gas for a tobacco dryer |
EP1249181A3 (en) * | 2001-04-10 | 2003-10-29 | British American Tobacco (Germany) GmbH | Treatment of process gas for a tobacco dryer |
US20050163968A1 (en) * | 2004-01-20 | 2005-07-28 | Hanket Gregory M. | Microfiller-reinforced polymer film |
US20070137259A1 (en) * | 2005-12-21 | 2007-06-21 | Borders Harley A | Processes and systems for making inorganic fibers |
US7802452B2 (en) * | 2005-12-21 | 2010-09-28 | Johns Manville | Processes for making inorganic fibers |
US20100319404A1 (en) * | 2005-12-21 | 2010-12-23 | Harley Allen Borders | Processes and systems for making inorganic fibers |
US8650915B2 (en) * | 2005-12-21 | 2014-02-18 | Johns Manville | Processes and systems for making inorganic fibers |
US20100147033A1 (en) * | 2006-01-10 | 2010-06-17 | Terry Joe Hanna | Method of fiberizing molten glass |
US9061936B2 (en) * | 2006-01-10 | 2015-06-23 | Johns Manville | Systems for fiberizing molten glass |
US20140076000A1 (en) * | 2012-09-20 | 2014-03-20 | Timothy James Johnson | Apparatus and method for air flow control during manufacture of glass fiber insulation |
US11572645B2 (en) * | 2017-09-01 | 2023-02-07 | Paroc Group Oy | Apparatus and method for manufacturing mineral wool as well as a mineral wool product |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3442633A (en) | Method and apparatus for conveying and for treating glass fibers | |
US3650716A (en) | Method of and apparatus for the production of fibers from thermoplastic materials, particularly glass fibers | |
US2707847A (en) | Means for treating mineral wool fibers | |
EP0878450B1 (en) | Scrap fiber refeed system and method | |
JP4927329B2 (en) | Filter media containing mineral fibers obtained by centrifugation | |
US5955011A (en) | Evaporative cooling apparatus and method for a fine fiber production process | |
HU225550B1 (en) | Processes and apparatus for producing synthetic vitreous fibre products | |
KR20070011318A (en) | Rotary separator for mineral fibers | |
CA1265342A (en) | Internal blower for expanding cylindrical veil of mineral fibers | |
US3532479A (en) | Apparatus for producing glass fibers | |
US3900302A (en) | Method for producing glass fiber bulk product | |
US4222757A (en) | Method for manufacturing glass fibers | |
US4321074A (en) | Method and apparatus for manufacturing glass fibers | |
US5322650A (en) | Method and apparatus for producing fibers | |
US2753598A (en) | Method for forming and collecting fibers | |
JP7244187B2 (en) | Method and apparatus for collecting fibers | |
US4508555A (en) | Method and apparatus for scrubbing effluent gases from mineral fiber production | |
US3142869A (en) | Process and apparatus for opening and cleaning fibrous material | |
US4298367A (en) | Method of and device for cleansing in a fibre blanket manufacturing plant | |
FI88018C (en) | ANORDNING VID FRAMSTAELLNING AV FIBER | |
US4140508A (en) | Method and apparatus for collecting strand formed from streams of molten material | |
US4595443A (en) | Pollution-reducing method of incorporating dust suppressant in fibrous insulation material | |
SU1006397A1 (en) | Method and apparatus for cleaning mineral wool from beads | |
CA1174050A (en) | Apparatus for the production of mineral fibers having rotating discs | |
KR820001156B1 (en) | Method for making fibers from thermoplastic materials |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: SCHULLER INTERNATIONAL, INC., COLORADO Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:CLOCKSIN, KENNETH ANDREW;CUSICK, MICHAEL J.;REEL/FRAME:008287/0302 Effective date: 19961018 |
|
AS | Assignment |
Owner name: JOHNS MANVILLE INTERNATIONAL, INC., COLORADO Free format text: CHANGE OF NAME;ASSIGNOR:SCHULLER INTERNATIONAL, INC.;REEL/FRAME:008581/0213 Effective date: 19970502 |
|
STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
FPAY | Fee payment |
Year of fee payment: 4 |
|
REMI | Maintenance fee reminder mailed | ||
FPAY | Fee payment |
Year of fee payment: 8 |
|
FPAY | Fee payment |
Year of fee payment: 12 |